CN106500406A - A kind of driving heat source sensible heat direct circulation utilizes type multistage evaporation enrichment facility - Google Patents
A kind of driving heat source sensible heat direct circulation utilizes type multistage evaporation enrichment facility Download PDFInfo
- Publication number
- CN106500406A CN106500406A CN201610936968.4A CN201610936968A CN106500406A CN 106500406 A CN106500406 A CN 106500406A CN 201610936968 A CN201610936968 A CN 201610936968A CN 106500406 A CN106500406 A CN 106500406A
- Authority
- CN
- China
- Prior art keywords
- evaporation
- heat exchanger
- condenser
- evaporator
- heat
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B30/00—Heat pumps
- F25B30/02—Heat pumps of the compression type
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B1/00—Compression machines, plants or systems with non-reversible cycle
- F25B1/10—Compression machines, plants or systems with non-reversible cycle with multi-stage compression
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B41/00—Fluid-circulation arrangements
- F25B41/30—Expansion means; Dispositions thereof
- F25B41/31—Expansion valves
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B41/00—Fluid-circulation arrangements
- F25B41/30—Expansion means; Dispositions thereof
- F25B41/37—Capillary tubes
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The present invention provides a kind of driving heat source sensible heat direct circulation using type multistage evaporation enrichment facility, and solving briquette boiler is used for energy waste and the environmental issue of concentrating streams.The present invention includes that the cascade high-temperature heat pump system hot lifting compressor of high-temperature level, high temperature nuclear one-stage throttling device, middle evaporative condenser, the hot lifting compressor of low-temperature level, low temperature nuclear one-stage throttling device and multistage evaporation concentration systems, multistage evaporation concentration systems include that primary combined type occurs condenser, flash evaporation, middle evaporation concentrators at different levels and end combined type condenser/evaporator.The present invention by high temperature heat pump reclaim concentration cooling water heat sensible heat direct circulation using system can significantly energy-conservation, the heat capacity of raising system and heating efficiency, notable than traditional its environmental benefit of Boiler Steam concentration systems.Through preliminary experiment data, not only can preferably solve boiler cooling water heat and waste the problems such as polluting with boiler coal, and plant running reliability, concentrating streams effect is significant.
Description
Technical field
The present invention relates to a kind of enrichment facility, particularly relates to a kind of driving heat source sensible heat direct circulation multistage using type
Evaporation concentration device.
Background technology
As industrial concentration technique develops, the development restriction of traditional utilization Boiler Steam concentrating streams is more and more brighter
Aobvious.First, the substantial amounts of coal of boiler combustion, causes environmental pollution.Secondly, the Boiler Steam waste heat for concentrating is potential substantial amounts of
Sensible heat, directly drains the waste for necessarily causing the energy.
Content of the invention
The present invention provides a kind of driving heat source sensible heat direct circulation and utilizes type multistage evaporation enrichment facility, to solve current coal
Charcoal boiler is used for the energy waste of concentrating streams and environmental issue.
The technical scheme is that and be achieved in that：A kind of driving heat source sensible heat direct circulation is dense using type multistage evaporation
Compression apparatus, steam including the cascade high-temperature heat pump system hot lifting compressor of high-temperature level, high temperature nuclear one-stage throttling device, centre
Send out-condenser, low-temperature level heat lifted use compressor, low temperature nuclear one-stage throttling device and multistage evaporation concentration systems, multistage evaporation concentrate
System includes the condensation-evaporation of primary combined type generation-condenser, flash evaporation, middle evaporation concentrators at different levels and end combined type
Device；The high-temperature level hot lifting compressor outlet is by primary combined type generations-condenser and corresponding connecting line and height
The corresponding entrance connection of warm nuclear one-stage throttling device, the high temperature nuclear one-stage throttling device outlet accesses the corresponding entrance of evaporator-condenser, described
Evaporator-condenser outlet entrance connection corresponding to the hot lifting compressor of high-temperature level, low temperature nuclear one-stage throttling device respectively, described
The outlet of low temperature nuclear one-stage throttling device is connected with an entrance of end combined type Condensation-Evaporator, end combined type condensation-evaporation
The one outlet of the device and low-temperature level hot lifting corresponding entrance connection of compressor, low-temperature level heat the liftings compressor outlet and
Another entrance of evaporator-condenser is connected；Described primary combined type generation-condensator outlet meets the entrance of flash evaporation, institute
State another entrance that flash evaporation connects end combined type Condensation-Evaporator by middle evaporation concentrators at different levels, end combined type
Another outlet of Condensation-Evaporator is connected with primary combined type generation-condenser inlet；Described centre evaporation and concentration at different levels
The head end heat exchanger of device taps into material mouth, and the end heat exchanger of middle evaporation concentrators at different levels picks out material mouth, and middle evaporations at different levels are dense
Each heat exchanger of contracting device is sequentially connected.
Centre evaporation concentrator at different levels includes that first order evaporation concentrator heat exchanger, first order evaporation concentrator are used
Vacuum plant, second level evaporation concentrator heat exchanger and second level evaporation concentrator vacuum plant；Described evaporimeter according to
Secondary by first order evaporation concentrator heat exchanger, first order evaporation concentrator vacuum plant, second level evaporation concentrator use
Heat exchanger and second level evaporation concentrator vacuum plant connect another entrance of end combined type Condensation-Evaporator；Described
Another entrance of one-level evaporation concentrator heat exchanger picks out material mouth, and another outlet of first order evaporation concentrator heat exchanger is led to
Cross second level evaporation concentrator heat exchanger and pick out material mouth.
The high temperature nuclear one-stage throttling device and low temperature nuclear one-stage throttling device are electric expansion valve, heating power expansion valve, capillary or section
Any one reducing pressure by regulating flow device in stream short tube.
The first order evaporation concentrator heat exchanger and second level evaporation concentrator heat exchanger are bushing type, space bar
Any one in formula, case tubular type, shell-tube type or composite heat exchanger.
The hot lifting compressor of the described high-temperature level by DC motor Driver and the hot lifting compressor of low-temperature level are living
Any one in plug, vortex, triangle rotor type compressor, and be enclosed in same closed shell with direct current generator.
Described end combined type Condensation-Evaporator is spray-type heat exchanger, primary combined type generation-condenser and steaming
Send out-condenser is bushing type, any one version in board-like or parallel-flow heat exchanger；First order evaporation concentrator is with changing
Hot device and second level evaporation concentrator heat exchanger are direct-contact heat exchanger.
A kind of driving heat source sensible heat direct circulation utilizes the method for concentration of type multistage evaporation enrichment facility, all the way cold-producing medium warp
The hot lifting of low-temperature level is discharged with exhaust outlet of compressor, sequentially passes through evaporator-condenser, low temperature nuclear one-stage throttling device, end combined type
After Condensation-Evaporator, sucked from entrance by the hot lifting compressor of low-temperature level；Another road cold-producing medium is through high-temperature level heat lifting pressure
Contracting machine exhaust outlet is discharged, and after sequentially passing through primary combined type generation-condenser, high temperature nuclear one-stage throttling device, evaporator-condenser, is entered
Enter the hot lifting compressor of high-temperature level；Also high-temperature steam is discharged into middle evaporation concentrator at different levels from flash evaporation all the way, most
End combined type Condensation-Evaporator first entrance is entered from the outlet of middle evaporation concentrators at different levels eventually and is condensed into low temperature liquid
Water, then the second entrance for being back to primary combined type generation-condenser from the first outlet of end combined type Condensation-Evaporator adds
Into high-temperature water, high-temperature water from primary combined type heat occurs-condenser second outlet exits into flash evaporation and flash into steam；Most
Afterwards, concentrating streams flow out heat exchanger through middle evaporation concentrators at different levels from charging aperture all the way, and concentrating streams are through being concentrated into
After desired concn, discharging opening is entered from the end heat exchanger outlet of middle evaporation concentrators at different levels.
During heretofore described steam sensible heat direct circulation is after recoverable concentration using system purpose, low temperature steams
Vapour waste heat, aids in concentrating streams or heat supply to recycle for boiler.Its principle is：By high temperature heat pump end composite type cold
Solidifying-evaporimeter, collects steam sensible heat, and the water for generating is cooled down.When waste heat recovery pattern is run, will be raw by water pump
Into water be sent to primary combined type generation-condenser and heat and carry out shwoot.
Beneficial effects of the present invention are as follows：
A kind of driving heat source sensible heat direct circulation that the present invention is provided utilizes type multistage evaporation enrichment facility.Returned by high temperature heat pump
Receive concentration cooling water heat sensible heat direct circulation using system can significantly energy-conservation, the heat capacity of raising system and heating efficiency,
Also, it is notable than traditional its environmental benefit of Boiler Steam concentration systems.Through studying the data obtained to preliminary experiment of the present invention,
The present invention not only can preferably solve boiler cooling water heat and waste the problems such as polluting with boiler coal, and plant running can
Lean on, concentrating streams effect is significant.The present invention is significant with application to the popularization of concentrating streams, is that driving heat source sensible heat is straight
Recycling type multistage evaporation concentration technique is connect there is provided technical support.
Description of the drawings
In order to be illustrated more clearly that the embodiment of the present invention or technical scheme of the prior art, below will be to embodiment or existing
Accompanying drawing to be used needed for having technology description is briefly described, it should be apparent that, drawings in the following description are only this
Some embodiments of invention, for those of ordinary skill in the art, on the premise of not paying creative work, can be with
Other accompanying drawings are obtained according to these accompanying drawings.
Fig. 1 is present configuration schematic diagram.
Fig. 2 is mode of operation flow chart of the present invention.
In figure：1 be the hot lifting compressor of high-temperature level, 2 be primary combined type generation-condenser, 3 be high-temperature level throttling dress
Put, 4 be evaporator-condenser, 5 be low temperature nuclear one-stage throttling device, 6 be end combined type Condensation-Evaporator, 7 be low-temperature level heat lifted
With compressor, 8 be flash evaporation, 9-1 be first order evaporation concentrator heat exchanger, 10-1 be second level evaporation concentrator heat exchange
Device, 9-2 first order evaporation and concentration vacuum plants, 10-2 be second level evaporation and concentration vacuum plant, 11-1 be the first pump,
It is the 3rd pump that 11-2 is the second pump, 11-3.
Specific embodiment
Accompanying drawing in below in conjunction with the embodiment of the present invention, to the embodiment of the present invention in technical scheme carry out clear, complete
Site preparation is described, it is clear that described embodiment is only a part of embodiment of the invention, rather than whole embodiment.It is based on
Embodiment in the present invention, it is every other that those of ordinary skill in the art are obtained under the premise of creative work is not paid
Embodiment, belongs to the scope of protection of the invention.
As shown in figure 1, the present invention provides a kind of driving heat source sensible heat direct circulation using type multistage evaporation enrichment facility, bag
Include the hot lifting compressor 1 of cascade high-temperature heat pump system high-temperature level, high temperature nuclear one-stage throttling device 3, centre evaporator-condenser
4th, low-temperature level heat is lifted and uses compressor 7, low temperature nuclear one-stage throttling device 5 and multistage evaporation concentration systems, multistage evaporation concentration systems bag
Include primary combined type generation-condenser 2, flash evaporation 8, middle evaporation concentrators at different levels and end combined type Condensation-Evaporator 6；
The high-temperature level heat is lifted with the outlet of compressor 1 by primary combined type generation-condenser 2 and corresponding connecting line and high temperature
3 corresponding entrance of nuclear one-stage throttling device connects, and the outlet of high temperature nuclear one-stage throttling device 3 accesses the corresponding entrance of evaporator-condenser 4, institute
The evaporator-condenser 4 that states is exported and is connected to the hot lifting compressor 1 of high-temperature level, 5 corresponding entrance of low temperature nuclear one-stage throttling device respectively,
The described outlet of low temperature nuclear one-stage throttling device 5 is connected with an entrance of end combined type Condensation-Evaporator 6, end combined type
The one outlet of Condensation-Evaporator 6 is lifted to low-temperature level heat and is connected with 7 corresponding entrance of compressor, and the low-temperature level heat is lifted to be used
The outlet of compressor 7 is connected with another entrance of evaporator-condenser 4；The described primary outlet of combined type generation-condenser 2 connects
The entrance of flash evaporation 8, the flash evaporation 8 meet the another of end combined type Condensation-Evaporator 6 by middle evaporation concentrators at different levels
Individual entrance, another outlet of end combined type Condensation-Evaporator 6 are connected with primary 2 entrance of combined type generation-condenser；Institute
The head end heat exchanger of the centre stated evaporation concentrator at different levels taps into material mouth, and the end heat exchanger of middle evaporation concentrators at different levels is picked out
Material mouth, each heat exchanger of middle evaporation concentrators at different levels are sequentially connected.
Centre evaporation concentrator at different levels includes that first order evaporation concentrator heat exchanger 9-1, the first order are concentrated by evaporation
Device vacuum plant 9-2, second level evaporation concentrator heat exchanger 10-1 and second level evaporation concentrator vacuum plant 10-2；
Described evaporimeter 8 passes sequentially through first order evaporation concentrator heat exchanger 9-1, first order evaporation concentrator vacuum plant 9-
2nd, second level evaporation concentrator heat exchanger 10-1 and second level evaporation concentrator vacuum plant 10-2 connect end composite type cold
Another entrance of solidifying-evaporimeter 6；Another entrance of the first order evaporation concentrator heat exchanger 9-1 picks out material mouth, and first
Another outlet of level evaporation concentrator heat exchanger 9-1 picks out material mouth by second level evaporation concentrator heat exchanger 10-1.
The high temperature nuclear one-stage throttling device 3 and low temperature nuclear one-stage throttling device 5 be electric expansion valve, heating power expansion valve, capillary or
Any one reducing pressure by regulating flow device in restriction sleeve.
The first order evaporation concentrator heat exchanger 9-1 and second level evaporation concentrator heat exchanger 10-1 are sleeve pipe
Formula, any one being spaced in board-like, case tubular type, shell-tube type or composite heat exchanger.
The hot lifting compressor 1 of the described high-temperature level by DC motor Driver and the hot lifting compressor 7 of low-temperature level are
Any one in piston type, vortex, triangle rotor type compressor, and be enclosed in same closed shell with direct current generator.
Described end combined type Condensation-Evaporator 6 is spray-type heat exchanger, primary combined type generations-condenser 2 and steaming
Send out-condenser 4 is bushing type, any one version in board-like or parallel-flow heat exchanger；First order evaporation concentrator is used
Heat exchanger 9-1 and second level evaporation concentrator heat exchanger 10-1 are direct-contact heat exchanger.
A kind of driving heat source sensible heat direct circulation utilizes the method for concentration of type multistage evaporation enrichment facility, all the way cold-producing medium warp
Low-temperature level heat is lifted is discharged with 7 exhaust outlet of compressor, is sequentially passed through evaporator-condenser 4, low temperature nuclear one-stage throttling device 5, end and is combined
After formula Condensation-Evaporator 6, sucked from entrance with compressor 7 by the hot lifting of low-temperature level；Another road cold-producing medium is lifted through high-temperature level heat
Discharged with 1 exhaust outlet of compressor, sequentially pass through primary combined type generation-condenser 2, high temperature nuclear one-stage throttling device 3, evaporation-condensation
After device 4, enter high-temperature level heat and lifted with compressor 1；Also high-temperature steam is discharged into middle evaporation at different levels from flash evaporation 8 all the way
Inspissator, finally enters 6 first entrance of end combined type Condensation-Evaporator from the outlet of middle evaporation concentrators at different levels and is condensed into
Low temperature liquid water, then primary combined type is back to by the 3rd pump 11-3 from the first outlet of end combined type Condensation-Evaporator 6
The second entrance of generation-condenser 2 is heated into high-temperature water, and high-temperature water occurs -2 second outlet of condenser outflow from primary combined type
Enter flash evaporation 8 and flash into steam；Finally, concentrating streams flow out changing through middle evaporation concentrators at different levels from charging aperture all the way
Hot device, concentrating streams are changed from the end of middle evaporation concentrators at different levels by the second pump 11-2 after being concentrated into desired concn
Hot device outlet enters discharging opening.
The principle of the present invention is as follows：Condensate from end combined type Condensation-Evaporator 6 enters superposition type by water pump
The 2 absorption refrigeration agent phase transformation heat of primary combined type generation-condenser of high temperature heat pump system, is changed into the aqueous water of HTHP,
Subsequently into 8 inner shwoot of flash evaporation, decrease temperature and pressure becomes the water of make a living steam and liquid, wherein gives birth to steam entrance first order evaporation dense
Contracting device is mixed with the material liquid for needing concentration with heat exchanger 9-1, releases heat, while absorbing the steaming of material liquid evaporation for the first time
Vapour is changed into indirect steam, then enters second level evaporation concentrator with changing through first order evaporation and concentration vacuum plant 9-2 again
Hot device 10-1, with from first order evaporation concentrator carried out with the material liquid of heat exchanger 9-1 secondary mix, release heat simultaneously
The steam for absorbing material liquid double evaporation-cooling is changed into three steam, most afterwards through middle second level evaporation concentrator vacuum plant 10-2
End combined type Condensation-Evaporator 6 is entered, and hot friendship is carried out with the cold-producing medium for coming from cascade high-temperature heat pump system hypothermia level
Change, release heat, be changed into the condensate of low-temp low-pressure, then start subsequent cycle through pump.Come from the material liquid warp of storeroom
First order evaporation concentrator is sprayed into heat exchanger 9-1 upper ends, is then absorbed heat with the raw steam from flash evaporation 8, is entered
Row is first to be concentrated by evaporation, and later falls into the bottom of first order evaporation concentrator heat exchanger 9-1, enters second level evaporation through pump dense
Contracting device heat exchanger 9-2 carries out double evaporation-cooling concentration, repeats said process, after the concentration of multistage evaporation inspissator, finally by
It is pumped between product.Come from the HTHP superheated refrigerant that the hot lifting compressor 1 of high-temperature level is discharged, enter primary compound
Heat released by formula generation-condenser 2 is used for condensate of the heating from end combined type Condensation-Evaporator 6, subsequently becomes saturation
Or the liquid high-pressure refrigerant of supercooling, it is changed into the gas-liquid two-phase refrigeration of low-temp low-pressure after 3 step-down of high temperature nuclear one-stage throttling device throttling
Agent, enters evaporation in evaporator-condenser 4 and absorbs the heat for coming from low-temperature level circulating refrigerant, be changed into overheated gaseous refrigerant
Agent, the air entry for finally entering the hot lifting compressor 1 of high-temperature level start subsequent cycle process；Come from low-temperature level heat and lift use
The HTHP superheated refrigerant that compressor 7 is discharged, in entrance evaporator-condenser 4, releasing heat comes from high-temperature level and follows
Ring cold-producing medium, is condensed into the liquid high pressure refrigerant of saturation or supercooling, after 5 reducing pressure by regulating flow of low temperature nuclear one-stage throttling device is changed into low temperature
The gas-liquid two-phase cold-producing medium of low pressure, enters end combined type Condensation-Evaporator 6 and absorbs and come from the steaming of afterbody evaporation concentrator
The heat of vapour, is changed into overheated gaseous refrigerant, and the air entry for finally entering the hot lifting compressor of low-temperature level starts next following
Ring process.
The mode of operation of the present invention is as follows：
As shown in Fig. 2 export hot for low-temperature level lifting compressor 7 connecting with 4 second entrance of evaporator-condenser, evaporation-condensation
4 second outlet of device is connected with 5 entrance of low temperature nuclear one-stage throttling device, and the outlet of low temperature nuclear one-stage throttling device 5 condenses-evaporation with end combined type
6 second entrance of device is connected, and end combined type 6 second outlet entrance low-temperature levels of Condensation-Evaporator are hot to be lifted with 7 air-breathing of compressor
Mouthful；Hot for high-temperature level lifting compressor 1 is exported and is connected with primary 2 first entrance of combined type generation-condenser, primary combined type
2 first outlet of generation-condenser is connected with 3 entrance of high temperature nuclear one-stage throttling device, and high temperature nuclear one-stage throttling device 3 is exported and evaporation-condensation
4 first entrance of device is connected, and 4 first outlet of evaporator-condenser enters high-temperature level heat and lifted with 1 entrance of compressor.
Cold-producing medium is discharged with 7 exhaust outlet of compressor through the hot lifting of low-temperature level all the way, sequentially passes through evaporator-condenser 4, low temperature
After nuclear one-stage throttling device 5, end combined type Condensation-Evaporator 6, sucked from entrance with compressor 7 by the hot lifting of low-temperature level；Another road
Cold-producing medium is discharged with 1 exhaust outlet of compressor through the hot lifting of high-temperature level, sequentially passes through primary combined type generation-condenser 2, high-temperature level
After throttling arrangement 3, evaporator-condenser 4, enter high-temperature level heat and lifted with compressor 1；Also all the way high-temperature steam from flash evaporation 8
It is discharged into first order evaporation concentrator heat exchanger 9-1 first entrances, then from first order evaporation concentrator heat exchanger 9-1
One outlet enters the first order and is concentrated by evaporation the entrance with vacuum plant 9-2, then from first order evaporation and concentration with vacuum plant 9-2's
Outlet enters first entrance of second level evaporation concentrator heat exchanger 10-1, from second level evaporation concentrator heat exchanger
The first outlet of 10-1 enters the second level and is concentrated by evaporation the entrance with vacuum plant 10-2, and high-temperature steam is through repeatedly heat exchange cooling
Afterwards, finally 6 first entrance of end combined type Condensation-Evaporator is entered from second level evaporation and concentration with the outlet of vacuum plant 10-2
It is condensed into low temperature liquid water, then primary is back to by the 3rd pump 11-3 from the first outlet of end combined type Condensation-Evaporator 6
The second entrance of combined type generation-condenser 2 is heated into high-temperature water, and high-temperature water occurs from primary combined type-and condenser 2 second goes out
Mouth exits into flash evaporation 8 and flashes into steam；Finally, concentrating streams are flowed out through first order evaporation concentrator from charging aperture all the way
With the second entrance of heat exchanger 9-1, the second outlet of first order evaporation concentrator heat exchanger 9-1 connects by the first pump 11-1
Second entrance of the dual evaporation inspissator with heat exchanger 10-1, concentrating streams after being concentrated into desired concn, by the second pump
11-2 enters discharging opening from second level evaporation concentrator with the second outlet of heat exchanger 10-1.
Presently preferred embodiments of the present invention is the foregoing is only, not in order to limit the present invention, all in essence of the invention
Within god and principle, any modification, equivalent substitution and improvements that is made etc. should be included within the scope of the present invention.
Claims (7)
1. a kind of driving heat source sensible heat direct circulation utilizes type multistage evaporation enrichment facility, it is characterised in that：High including superposition type
The hot lifting compressor of temperature heat pump system high-temperature level（1）, high temperature nuclear one-stage throttling device（3）, centre evaporator-condenser（4）, low
Warm level heat lifting compressor（7）, low temperature nuclear one-stage throttling device（5）With multistage evaporation concentration systems, multistage evaporation concentration systems bag
Include primary combined type generation-condenser（2）, flash evaporation（8）, middle evaporation concentrators at different levels and end combined type condensation-evaporation
Device（6）；The high-temperature level heat lifting compressor（1）Outlet is by primary combined type generation-condenser（2）And corresponding connection
Pipeline and high temperature nuclear one-stage throttling device（3）Corresponding entrance connection, the high temperature nuclear one-stage throttling device（3）Outlet accesses evaporator-condenser
（4）Corresponding entrance, described evaporator-condenser（4）Outlet respectively with the hot lifting compressor of high-temperature level（1）, low-temperature level section
Stream device（5）Corresponding entrance connection, described low temperature nuclear one-stage throttling device（5）Outlet and end combined type Condensation-Evaporator（6）'s
One entrance is connected, end combined type Condensation-Evaporator（6）One outlet and low-temperature level heat lifting compressor（7）Phase
Entrance is answered to connect, the low-temperature level heat lifting compressor（7）Outlet and evaporator-condenser（4）Another entrance be connected；Institute
The primary combined type generation-condenser that states（2）Outlet connects flash evaporation（8）Entrance, the flash evaporation（8）By middle steamings at different levels
Send out inspissator and connect end combined type Condensation-Evaporator（6）Another entrance, end combined type Condensation-Evaporator（6）Another
Outlet and primary combined type generation-condenser（2）Entrance is connected；The head end heat exchanger of described centre evaporation concentrator at different levels
Material mouth is tapped into, the end heat exchanger of middle evaporation concentrators at different levels picks out material mouth, each heat exchanger of middle evaporation concentrators at different levels
It is sequentially connected.
2. a kind of driving heat source sensible heat direct circulation according to claim 1 utilizes type multistage evaporation enrichment facility, and which is special
Levy and be：Centre evaporation concentrator at different levels includes first order evaporation concentrator heat exchanger（9-1）, the first order be concentrated by evaporation
Device vacuum plant（9-2）, second level evaporation concentrator heat exchanger（10-1）With second level evaporation concentrator vacuum plant
（10-2）；Described evaporimeter（8）Pass sequentially through first order evaporation concentrator heat exchanger（9-1）, first order evaporation concentrator
Use vacuum plant（9-2）, second level evaporation concentrator heat exchanger（10-1）With second level evaporation concentrator vacuum plant
（10-2）Connect end combined type Condensation-Evaporator（6）Another entrance；The first order evaporation concentrator heat exchanger（9-
1）Another entrance pick out material mouth, first order evaporation concentrator heat exchanger（9-1）Another outlet evaporated by the second level dense
Contracting device heat exchanger（10-1）Pick out material mouth.
3. a kind of driving heat source sensible heat direct circulation according to claim 1 utilizes type multistage evaporation enrichment facility, and which is special
Levy and be：The high temperature nuclear one-stage throttling device（3）With low temperature nuclear one-stage throttling device（5）For electric expansion valve, heating power expansion valve, capillary
Or any one the reducing pressure by regulating flow device in restriction sleeve.
4. a kind of driving heat source sensible heat direct circulation according to claim 2 utilizes type multistage evaporation enrichment facility, and which is special
Levy and be：The first order evaporation concentrator heat exchanger（9-1）With second level evaporation concentrator heat exchanger（10-1）For set
Tubular type, any one being spaced in board-like, case tubular type, shell-tube type or composite heat exchanger.
5. a kind of driving heat source sensible heat direct circulation according to claim 1 utilizes type multistage evaporation enrichment facility, and which is special
Levy and be：The hot lifting compressor of the described high-temperature level by DC motor Driver（1）With the hot lifting compressor of low-temperature level（7）
For any one in piston type, vortex, triangle rotor type compressor, and same closed shell is enclosed in direct current generator
Interior.
6. a kind of driving heat source sensible heat direct circulation according to claim 2 utilizes type multistage evaporation enrichment facility, and which is special
Levy and be：Described end combined type Condensation-Evaporator（6）For spray-type heat exchanger, primary combined type generation-condenser（2）
And evaporator-condenser（4）For any one version in bushing type, board-like or parallel-flow heat exchanger；First order evaporation is dense
Contracting device heat exchanger（9-1）With second level evaporation concentrator heat exchanger（10-1）For direct-contact heat exchanger.
7. in a kind of employing claim 1-6, arbitrary driving heat source sensible heat direct circulation utilizes the dense of type multistage evaporation enrichment facility
Compression method, it is characterised in that：Cold-producing medium is through the hot lifting compressor of low-temperature level all the way（7）Exhaust outlet discharge, sequentially pass through evaporation-
Condenser（4）, low temperature nuclear one-stage throttling device（5）, end combined type Condensation-Evaporator（6）Afterwards, by the hot lifting compressor of low-temperature level
（7）Suck from entrance；Another road cold-producing medium is through the hot lifting compressor of high-temperature level（1）Exhaust outlet is discharged, and is sequentially passed through primary multiple
Box-like generation-condenser（2）, high temperature nuclear one-stage throttling device（3）, evaporator-condenser（4）Afterwards, high-temperature level heat lifting compression is entered
Machine（1）；Also all the way high-temperature steam from flash evaporation（8）Middle evaporation concentrator at different levels is discharged into, finally from middle steamings at different levels
The outlet for sending out inspissator enters end combined type Condensation-Evaporator（6）First entrance is condensed into low temperature liquid water, then multiple from end
Box-like Condensation-Evaporator（6）First outlet be back to primary combined type generation-condenser（2）Second entrance be heated into height
Warm water, high-temperature water is from primary combined type generation-condenser（2）Second outlet exits into flash evaporation（8）Flash into steam；Most
Afterwards, concentrating streams flow out heat exchanger through middle evaporation concentrators at different levels from charging aperture all the way, and concentrating streams are through being concentrated into
After desired concn, discharging opening is entered from the end heat exchanger outlet of middle evaporation concentrators at different levels.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610936968.4A CN106500406B (en) | 2016-10-25 | 2016-10-25 | A kind of driving heat source sensible heat direct circulation utilizes type multistage evaporation enrichment facility |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610936968.4A CN106500406B (en) | 2016-10-25 | 2016-10-25 | A kind of driving heat source sensible heat direct circulation utilizes type multistage evaporation enrichment facility |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106500406A true CN106500406A (en) | 2017-03-15 |
| CN106500406B CN106500406B (en) | 2018-10-16 |
Family
ID=58320009
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610936968.4A Active CN106500406B (en) | 2016-10-25 | 2016-10-25 | A kind of driving heat source sensible heat direct circulation utilizes type multistage evaporation enrichment facility |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106500406B (en) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0042605A1 (en) * | 1980-06-20 | 1981-12-30 | A/S Niro Atomizer | Method of operating a vapour-heated process system |
| JP2003106702A (en) * | 2001-09-26 | 2003-04-09 | Daikin Ind Ltd | Absorption refrigerating machine |
| CN1535920A (en) * | 2003-04-03 | 2004-10-13 | 孙伯鲁 | Sea water desalination equipment capable of simulating natural rainfall |
| CN1546386A (en) * | 2003-12-16 | 2004-11-17 | 国家海洋局天津海水淡化与综合利用研 | Method and device for desalting sea water using mechanical compression distillation method |
| CN202229469U (en) * | 2011-08-30 | 2012-05-23 | 福建成信绿集成有限公司 | Compression heat pump system with liquid dehumidifying function |
-
2016
- 2016-10-25 CN CN201610936968.4A patent/CN106500406B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0042605A1 (en) * | 1980-06-20 | 1981-12-30 | A/S Niro Atomizer | Method of operating a vapour-heated process system |
| JP2003106702A (en) * | 2001-09-26 | 2003-04-09 | Daikin Ind Ltd | Absorption refrigerating machine |
| CN1535920A (en) * | 2003-04-03 | 2004-10-13 | 孙伯鲁 | Sea water desalination equipment capable of simulating natural rainfall |
| CN1546386A (en) * | 2003-12-16 | 2004-11-17 | 国家海洋局天津海水淡化与综合利用研 | Method and device for desalting sea water using mechanical compression distillation method |
| CN202229469U (en) * | 2011-08-30 | 2012-05-23 | 福建成信绿集成有限公司 | Compression heat pump system with liquid dehumidifying function |
Also Published As
| Publication number | Publication date |
|---|---|
| CN106500406B (en) | 2018-10-16 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104964477B (en) | A kind of multistage plate evaporation absorption type refrigerating unit and method | |
| CN106492491A (en) | A kind of driving heat source latent heat indirect cyclic process utilizes type multistage evaporation enrichment facility | |
| CN101949609B (en) | Low-temperature heat source-driven air-cooling ammonia water absorption refrigerating machine | |
| CN107036324A (en) | A kind of weary wind source heat pump equipment system based on heat pipe heat exchanging | |
| CN103994486B (en) | The efficient heating system of the big temperature difference of gas fired-boiler | |
| CN201884080U (en) | Steam exhaust waste heat recycling unit | |
| CN102022145A (en) | Steam exhaust waste heat recovery unit | |
| CN103322727A (en) | Heat pump system as well as drying system and method | |
| CN102322705A (en) | Circulating device combining diffusing absorption-type refrigeration and vapor compression refrigeration | |
| CN107144042A (en) | A kind of second-kind absorption-type heat pump | |
| CN202470543U (en) | Warming type absorption heat pump with middle-temperature heat source in series | |
| CN110030758A (en) | A kind of big temperature difference absorption heat pump of multi-stage, efficient and absorption heat exchange device | |
| CN105650938B (en) | A kind of absorption-type refrigerating method and device of full electric power reuse discharge heat | |
| CN102840719B (en) | Solar energy air source absorption heat pump device | |
| CN217178934U (en) | Efficient lithium bromide compression absorption type combined circulation system | |
| CN106568236B (en) | Hot direct circulation utilizes type multistage evaporation enrichment facility entirely for a kind of driving heat source | |
| CN207620863U (en) | A kind of Organic Rankine Cycle power generator | |
| CN206094279U (en) | Slaughterhouse is with multistage full heat recovery hot water system of refrigerating unit | |
| CN111336720B (en) | Full-water-cooling segregation ammonia absorption heat pump system and control method | |
| CN106500406A (en) | A kind of driving heat source sensible heat direct circulation utilizes type multistage evaporation enrichment facility | |
| CN204612241U (en) | Biomass direct-fired cold/hot water machine of lithium bromide group | |
| CN107461799A (en) | A kind of heating equipment and heat supply method | |
| CN208635172U (en) | A kind of water source heat pump heat supply system with recuperation of heat | |
| CN209054541U (en) | A kind of eliminating white smoke system | |
| CN202521939U (en) | Heat pump system and drying system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP02 | Change in the address of a patent holder | ||
| CP02 | Change in the address of a patent holder |
Address after: 451191 No. 1 Huaihe Road, Shuang Hu Economic and Technological Development Zone, Xinzheng, Zhengzhou, Henan Patentee after: Zhongyuan University of Technology Address before: 451191 No. 1 Huaihe Road, Shuanghu Town Economic and Technological Development Zone, Zhengzhou City, Henan Province Patentee before: Zhongyuan University of Technology |